TW202045753A - Cyclic epitaxy deposition system - Google Patents
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- C30B25/00—Single-crystal growth by chemical reaction of reactive gases, e.g. chemical vapour-deposition growth
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45523—Pulsed gas flow or change of composition over time
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45523—Pulsed gas flow or change of composition over time
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- C23C16/45548—Atomic layer deposition [ALD] characterized by the apparatus having arrangements for gas injection at different locations of the reactor for each ALD half-reaction
- C23C16/45551—Atomic layer deposition [ALD] characterized by the apparatus having arrangements for gas injection at different locations of the reactor for each ALD half-reaction for relative movement of the substrate and the gas injectors or half-reaction reactor compartments
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45561—Gas plumbing upstream of the reaction chamber
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/455—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
- C23C16/45563—Gas nozzles
- C23C16/45565—Shower nozzles
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/46—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for heating the substrate
- C23C16/463—Cooling of the substrate
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- C23C16/00—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
- C23C16/44—Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
- C23C16/54—Apparatus specially adapted for continuous coating
- C23C16/545—Apparatus specially adapted for continuous coating for coating elongated substrates
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- C30B25/00—Single-crystal growth by chemical reaction of reactive gases, e.g. chemical vapour-deposition growth
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- C30B25/00—Single-crystal growth by chemical reaction of reactive gases, e.g. chemical vapour-deposition growth
- C30B25/02—Epitaxial-layer growth
- C30B25/14—Feed and outlet means for the gases; Modifying the flow of the reactive gases
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- H01—ELECTRIC ELEMENTS
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- H01J37/00—Discharge tubes with provision for introducing objects or material to be exposed to the discharge, e.g. for the purpose of examination or processing thereof
- H01J37/32—Gas-filled discharge tubes
- H01J37/32431—Constructional details of the reactor
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- H01J2237/00—Discharge tubes exposing object to beam, e.g. for analysis treatment, etching, imaging
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- H01J2237/32—Processing objects by plasma generation
- H01J2237/33—Processing objects by plasma generation characterised by the type of processing
- H01J2237/332—Coating
- H01J2237/3321—CVD [Chemical Vapor Deposition]
Abstract
Description
本發明涉及一種磊晶沉積系統,特別是涉及一種利用原子層沉積原理的循環式磊晶沉積系統。The invention relates to an epitaxial deposition system, in particular to a cyclic epitaxial deposition system using the principle of atomic layer deposition.
原子層沉積(atomic layer deposition)是以氣相方式來成長高品質薄膜的技術。相較於以化學氣相沉積或者是物理氣相沉積所形成的膜層而言,利用原子層沉積所形成的膜層具有更高的緻密性、厚度均勻性以及階梯覆蓋率。另外,利用原子層沉積可精密地控制膜層厚度。因此,原子層沉積技術已經被應用在電子元件的製造流程中。Atomic layer deposition is a technology for growing high-quality thin films in a vapor phase. Compared with the film formed by chemical vapor deposition or physical vapor deposition, the film formed by atomic layer deposition has higher density, thickness uniformity and step coverage. In addition, the thickness of the film can be precisely controlled by atomic layer deposition. Therefore, atomic layer deposition technology has been applied in the manufacturing process of electronic components.
在原子層沉積時,在每一次鍍膜循環(cycle)中,兩種不同的前驅物氣體是在不同的時間點依序通入鍍膜腔體,而非同時間通入鍍膜腔體內。每次所通入的前驅物氣體與基材表面發生自限性(self-limiting)反應,而只形成單原子層。在多次鍍膜循環之後,才會形成具有特定厚度的膜層。During atomic layer deposition, in each coating cycle, two different precursor gases are sequentially passed into the coating chamber at different time points instead of entering the coating chamber at the same time. Each time the introduced precursor gas undergoes a self-limiting reaction with the surface of the substrate, and only a single atomic layer is formed. After multiple coating cycles, a film with a specific thickness is formed.
因此,相對於化學氣相沉積,利用原子層沉積的製程時間較長,且目前無法應用於連續式生產,而不適合應用於製造需要大量生產的元件或裝置。Therefore, compared with chemical vapor deposition, the process time of using atomic layer deposition is longer, and it cannot be applied to continuous production at present, and is not suitable for manufacturing components or devices that require mass production.
本發明所要解決的技術問題在於,提供一種循環式磊晶沉積系統,以縮短利用原子層沉積技術的沉積時間。The technical problem to be solved by the present invention is to provide a cyclic epitaxial deposition system to shorten the deposition time using atomic layer deposition technology.
為了解決上述的技術問題,本發明所採用的其中一技術方案是,提供一種循環式磊晶沉積系統,其包括鍍膜腔體、輸送裝置以及氣體分流模組。輸送裝置用以沿著一傳輸路徑連續地輸送一基材進出所述鍍膜腔體。氣體分流模組設置於鍍膜腔體內,並位於傳輸路徑上方。氣體分流模組包括彼此不連通的多個前驅物氣體噴嘴以及多個沖洗氣體噴嘴,以在同一時間將至少一前驅物氣體以及至少一沖洗氣體分別導引至基材上的不同區域。In order to solve the above technical problems, one of the technical solutions adopted by the present invention is to provide a circulating epitaxial deposition system, which includes a coating chamber, a conveying device, and a gas splitting module. The conveying device is used for continuously conveying a substrate in and out of the coating cavity along a conveying path. The gas splitting module is arranged in the coating cavity and above the transmission path. The gas splitting module includes a plurality of precursor gas nozzles and a plurality of flushing gas nozzles that are not connected to each other, so as to guide at least one precursor gas and at least one flushing gas to different areas on the substrate at the same time.
本發明的其中一有益效果在於,本發明所提供的循環式磊晶沉積系統,其能通過“輸送裝置用以沿著一傳輸路徑連續地輸送一基材進出所述鍍膜腔體”以及“氣體分流模組包括彼此不連通的多個前驅物氣體噴嘴以及多個沖洗氣體噴嘴,以在同一時間將至少一前驅物氣體以及至少一沖洗氣體分別導引至基材上的不同區域”的技術方案,以連續地在基材上形成膜層,可縮短沉積時間,並適合應用於製造需要大量生產的元件或者裝置。One of the beneficial effects of the present invention is that the circulating epitaxial deposition system provided by the present invention can be used to continuously transport a substrate along a transport path into and out of the coating chamber through a “transport device” and “gas The splitter module includes a plurality of precursor gas nozzles and a plurality of flushing gas nozzles that are not connected to each other, so as to guide at least one precursor gas and at least one flushing gas to different areas on the substrate at the same time." , To continuously form a film layer on the substrate, which can shorten the deposition time, and is suitable for manufacturing components or devices that require mass production.
為使能更進一步瞭解本發明的特徵及技術內容,請參閱以下有關本發明的詳細說明與圖式,然而所提供的圖式僅用於提供參考與說明,並非用來對本發明加以限制。In order to further understand the features and technical content of the present invention, please refer to the following detailed description and drawings about the present invention. However, the provided drawings are only for reference and description, and are not used to limit the present invention.
以下是通過特定的具體實施例來說明本發明所公開有關“循環式磊晶沉積系統”的實施方式,本領域技術人員可由本說明書所公開的內容瞭解本發明的優點與效果。本發明可通過其他不同的具體實施例加以施行或應用,本說明書中的各項細節也可基於不同觀點與應用,在不悖離本發明的構思下進行各種修改與變更。另外,本發明的附圖僅為簡單示意說明,並非依實際尺寸的描繪,事先聲明。以下的實施方式將進一步詳細說明本發明的相關技術內容,但所公開的內容並非用以限制本發明的保護範圍。The following is a specific embodiment to illustrate the implementation of the "circular epitaxial deposition system" disclosed in the present invention. Those skilled in the art can understand the advantages and effects of the present invention from the content disclosed in this specification. The present invention can be implemented or applied through other different specific embodiments, and various details in this specification can also be modified and changed based on different viewpoints and applications without departing from the concept of the present invention. In addition, the drawings of the present invention are merely schematic illustrations, and are not drawn according to actual dimensions, and are stated in advance. The following embodiments will further describe the related technical content of the present invention in detail, but the disclosed content is not intended to limit the protection scope of the present invention.
應當可以理解的是,雖然本文中可能會使用到“第一”、“第二”、“第三”等術語來描述各種元件,但這些元件不應受這些術語的限制。這些術語主要是用以區分一元件與另一元件。另外,本文中所使用的術語“或”,應視實際情況可能包括相關聯的列出項目中的任一個或者多個的組合。It should be understood that although terms such as “first”, “second”, and “third” may be used herein to describe various elements, these elements should not be limited by these terms. These terms are mainly used to distinguish one element from another. In addition, the term "or" used in this document may include any one or a combination of more of the associated listed items depending on the actual situation.
請參照圖1。圖1顯示本發明實施例的循環式磊晶沉積系統的示意圖。須說明的是,本發明實施例的循環式磊晶沉積系統M1是以原子層沉積(或原子層磊晶)的原理,在一基材S1上形成特定膜層,如:鉑層、氧化鋁層、氧化鎳層、氧化錫層、氧化鈦層、氧化鐵層、氧化鋅層、磷鋰氮氧化物層(LiPON)、氮化鈦層等。另外,本發明實施例的循環式磊晶沉積系統M1可應用於卷對卷連續製程。Please refer to Figure 1. FIG. 1 shows a schematic diagram of a cyclic epitaxial deposition system according to an embodiment of the present invention. It should be noted that the cyclic epitaxial deposition system M1 of the embodiment of the present invention is based on the principle of atomic layer deposition (or atomic layer epitaxy) to form a specific film layer on a substrate S1, such as platinum layer, aluminum oxide Layer, nickel oxide layer, tin oxide layer, titanium oxide layer, iron oxide layer, zinc oxide layer, phosphorus lithium oxynitride layer (LiPON), titanium nitride layer, etc. In addition, the cyclic epitaxial deposition system M1 of the embodiment of the present invention can be applied to a continuous roll-to-roll process.
如圖1所示,循環式磊晶沉積系統M1至少包括一真空設備1。真空設備1包括一主腔體10、一鍍膜腔體11、一前處理腔體12、一輸送裝置13以及一抽氣裝置14。As shown in FIG. 1, the circulating epitaxial deposition system M1 includes at least one vacuum device 1. The vacuum equipment 1 includes a
鍍膜腔體11與前處理腔體12都設置在主腔體10內,並且定義出各自獨立的空間,以避免通入前處理腔體12內的氣體與通入鍍膜腔體11內的氣體相互擴散。在一實施例中,鍍膜腔體11的兩相反側分別具有允許基材S1進出的開口(圖未示)。The
輸送裝置13用以沿著一傳輸路徑連續地輸送基材S1通過前處理腔體12以及鍍膜腔體11。進一步而言,前處理腔體12以及鍍膜腔體11是設置在基材S1的傳輸路徑上。通過輸送裝置13連續式地傳送基材S1,基材S1的不同區段,也就是位於前處理腔體12內的區段以及位於鍍膜腔體11內的區段,可同時進行前處理以及膜層沉積。The
輸送裝置13包括一第一收放料模組13a以及一第二收放料模組13b,且第一收放料模組13a以及一第二收放料模組13b定義出基材S1的傳輸路徑。詳細而言,基材S1通過第一收放料模組13a的帶動,而連續地被傳送至前處理腔體12以及鍍膜腔體11內,且由鍍膜腔體11傳送出的基材S1通過第二收放料模組13b的帶動而被捲收。The
在本實施例中,第一收放料模組13a可包括第一收放料輪以及連接於第一收放料輪軸心的第一驅動元件。相似地,第二收放料模組13b可包括第二收放料輪以及連接於第二收放料輪軸心的第二驅動元件。In this embodiment, the first unwinding and unwinding
第一驅動元件以及第二驅動元件接受控制模組的指令,以在同時間分別驅動第一收放料輪與第二收放料輪(以順時針方向)轉動,以使捲繞在第一收放料輪上的基材S1被連續地傳送至前處理腔體12以及鍍膜腔體11。The first driving element and the second driving element receive instructions from the control module to respectively drive the first retracting and unwinding wheel and the second retracting and unwinding wheel (in a clockwise direction) to rotate at the same time, so that the winding is in the first The substrate S1 on the rewinding and unwinding wheel is continuously transferred to the
另外,第一收放料模組13a並可選擇性地包括一第一導向輪,以改變基材S1的輸送方向。相似地,第二收放料模組13b可選擇性地包括一第二導向輪,以改變由鍍膜腔體11傳送出的基材S1的行進方向。In addition, the first retracting and unwinding
須說明的是,在本實施例中,第一收放料模組13a以及第二收放料模組13b也可以改變基材S1的移動方向。具體而言,第一驅動元件與第二驅動元件接受控制模組的指令,以驅動第一收放料輪與第二收放料輪反向(逆時針)轉動,以使基材S1可在鍍膜腔體11內往復移動。如此,可在鍍膜腔體內重複進行多次鍍膜循環,而形成多層分子層於基材S1上。It should be noted that in this embodiment, the first retracting and unwinding
然而,本發明實施例的輸送裝置13並不以此為限。在另一實施例中,輸送裝置13包括一傳送帶,可連續地輸送待鍍工件進出前處理腔體12以及鍍膜腔體11。However, the
請參照圖1,在本發明實施例的循環式磊晶沉積系統M1中,基材S1在進入鍍膜腔體11之前,會先進入前處理腔體12內,以進行表面處理。據此,前處理腔體12與鍍膜腔體11依照基材S1的一移動方向依序設置於傳輸路徑上,且彼此隔離。1, in the cyclic epitaxial deposition system M1 of the embodiment of the present invention, before the substrate S1 enters the
另外,循環式磊晶沉積系統M1還進一步包括位於前處理腔體12內的一電漿裝置120。在一實施例中,可在前處理腔體12內通入氧氣、氮氣或者氬氣,以產生氧氣電漿、氮氣電漿或者氬氣電漿。如此,當基材S1被連續地傳送至前處理腔體12內時,通過電漿裝置120產生的電漿可對基材S1的表面進行表面處理。前述的表面處理例如是清潔基材S1的表面或者是增加基材S1表面的官能基。In addition, the circulating epitaxial deposition system M1 further includes a plasma device 120 located in the
另外,本實施例的循環式磊晶沉積系統M1,還進一步包括一前處理加熱模組121,其設置在前處理腔體12內並對應於傳輸路徑設置,以對基材S1加熱。須說明的是,前處理腔體12以及電漿裝置120為選擇性的元件,在其他實施例中,前處理腔體12以及電漿裝置120也可被省略。In addition, the circulating epitaxial deposition system M1 of this embodiment further includes a
通過輸送裝置13的帶動,經過表面處理之後的基材S1可由前處理腔體12移動至鍍膜腔體11內,以進行膜層沉積。請參照圖1以及圖2,圖2顯示本發明實施例的氣體分流模組的示意圖。Driven by the
氣體分流模組110設置於鍍膜腔體11內,並位於傳輸路徑上方。須說明的是,圖1所繪示的系統圖僅作為示例,並非用以限制電漿裝置120與氣體分流模組110之間的配置。在一實施例中,前處理腔體12中的電漿裝置120與氣體分流模組110是沿著一水平方向設置。在另一實施例中,電漿裝置120與氣體分流模組110的設置方向形成一夾角。也就是說,基材S1在前處理腔體12內的待處理表面,與基材S1在鍍膜腔體11內的另一部分待處理表面會分別面向不同方向。The
氣體分流模組110包括彼此不連通的多個前驅物氣體噴嘴110a、110c以及至少一沖洗氣體噴嘴110b(圖中繪示多個為例),以在同一時間將至少一前驅物氣體以及至少一沖洗氣體分別導引至基材S1上的不同區域。The
也就是說,在本發明實施例的循環式磊晶沉積系統M1中,不同的前驅物氣體以及沖洗氣體是在同時間,分別通過對應的前驅物氣體噴嘴110a、110c以及對應的沖洗氣體噴嘴110b通入鍍膜腔體11內。That is, in the cyclic epitaxial deposition system M1 of the embodiment of the present invention, different precursor gases and flushing gases pass through the corresponding
在本實施例中,多個前驅物氣體噴嘴110a、110c包括用以導引一第一前驅物氣體的一第一前驅物氣體噴嘴110a,以及用以導引一第二前驅物氣體的一第二前驅物氣體噴嘴110c。第一前驅物氣體以及第二前驅物氣體可以分別是不同種類的氣體,以在基材S1上形成單分子層(monolayer)。舉例而言,若要在基材S1上形成氮化鈦層,第一前驅物氣體為四氯化鈦(TiCl4
),第二前驅物氣體為氨氣(NH3
),而沖洗氣體為惰性氣體,如:氬氣(Ar)。In this embodiment, the plurality of
圖1的實施例中,繪示三個氣體分流模組110為例來進行說明。另外,每一個氣體分流模組110可包括多個噴嘴(圖1繪示6個為例),多個噴嘴至少包括一第一前驅物氣體噴嘴110a、至少一沖洗氣體噴嘴110b以及至少一第二前驅物氣體噴嘴110c,且第一前驅物氣體噴嘴110a、沖洗氣體噴嘴110b以及第二前驅物氣體噴嘴110c是沿著基材S1的一移動方向依序設置在傳輸路徑上方。In the embodiment of FIG. 1, three
據此,當基材S1被連續式地傳送時,基材S1的其中一特定區域會依序通過第一前驅物氣體噴嘴110a、沖洗氣體噴嘴110b以及第二前驅物氣體噴嘴110c下方,以完成一次鍍膜循環,而在該特定區域上形成一層單分子層。據此,當基材S1被帶動,而使該特定區域移動經過多個氣體分流模組110的下方之後,可在該特定區域上形成多層單分子層。在圖1以及圖2的實施例中,當基材S1連續式地通過所有氣體分流模組110下方之後,會完成六次鍍膜循環。Accordingly, when the substrate S1 is continuously conveyed, a specific area of the substrate S1 will sequentially pass under the first
也就是說,本發明實施例的循環式磊晶沉積系統M1基本上仍是利用原子層沉積原理,以在基材S1上形成膜層。然而,與現有的原子層沉積設備不同之處在於,本發明的實施例的循環式磊晶沉積系統M1中,利用輸送裝置13帶動基材S1移動,以及利用氣體分流模組110,可在同一時間在基材S1的不同區域通入每次鍍膜循環中所需要的前驅物氣體。In other words, the cyclic epitaxial deposition system M1 of the embodiment of the present invention basically still uses the principle of atomic layer deposition to form a film on the substrate S1. However, the difference from the existing atomic layer deposition equipment is that in the circulating epitaxial deposition system M1 of the embodiment of the present invention, the conveying
須說明的是,每一氣體分流模組110中,前驅物氣體噴嘴110a、110c的數量以及沖洗氣體噴嘴110b的數量並不以此為限,但是多個前驅物氣體噴嘴(第一前驅物氣體噴嘴110a以及第二前驅物氣體噴嘴110c)以及多個沖洗氣體噴嘴110b會交替設置。It should be noted that in each
在一實施例中,若在每一次鍍膜循環中,所要形成的單分子層需要三種前驅物氣體,則氣體分流模組110還可包括三個前驅物氣體噴嘴。也就是說,氣體分流模組110至少會包括第一前驅物氣體噴嘴、第二前驅物氣體噴嘴以及第三前驅物氣體噴嘴,且第一、第二以及第三前驅物氣體噴嘴會根據基材S1的移動方向,依序設置在傳輸路徑上方。因此,本發明實施例並不限制前驅物氣體噴嘴的數量。In an embodiment, if the monolayer to be formed requires three precursor gases in each coating cycle, the
前驅物氣體可通過對應的前驅物氣體噴嘴110a、110c,以在基材S1上方形成前驅物氣體分布區,兩個前驅物氣體噴嘴110a、110c分別在基材S1上所形成的兩個前驅物氣體分布區不重疊。請參照圖2,詳細而言,第一前驅物氣體以及第二前驅物氣體,可分別通過對應的第一前驅物氣體噴嘴110a以及第二前驅物氣體噴嘴110c,以在基材S1的不同區域上方形成第一前驅物氣體分布區P1以及第二前驅物氣體分布區P2。第一前驅物氣體分布區P1以及第二前驅物氣體分布區P2彼此不重疊。如此,可避免第一前驅物氣體在吸附到基材S1上之前,就與第二前驅物氣體相互擴散。The precursor gas can pass through the corresponding
相似地,沖洗氣體通過對應的沖洗氣體噴嘴110b,以在基材S1上方形成一沖洗氣體分布區P3,且兩個前驅物氣體分布區(第一前驅物氣體分布區P1以及第二前驅物氣體分布區P2)之間至少相隔一沖洗氣體分布區。換言之,沖洗氣體分布區P3是位於第一前驅物氣體分布區P1以及第二前驅物氣體分布區P2之間。沖洗氣體可去除基材S1上方多餘的第一前驅物氣體,且可選擇惰性氣體,如:氬氣。Similarly, the flushing gas passes through the corresponding flushing
另外,每一前驅物氣體噴嘴(第一前驅物氣體噴嘴110a以及第二前驅物氣體噴嘴110c)的底部的寬度由上向下漸縮,以使通過噴口流出的前驅物氣體可快速地被傳送至基材S1表面。在一實施例中,前驅物氣體噴嘴110a、110c的噴口與基材S1的表面之間的最短垂直距離d是介於0.1cm至2.0cm之間。如此,可避免前驅物氣體在噴灑到基材S1上之前往水平方向擴散。In addition, the width of the bottom of each precursor gas nozzle (the first
如圖1以及2所示,本發明實施例的循環式磊晶沉積系統M1,還進一步包括一加熱模組111。加熱模組111設置在鍍膜腔體11內,並位於傳輸路徑下方,以將基材S1加熱至特定的反應溫度。在本實施例中,加熱模組111包括多個加熱器111a~111c,可在同一時間分別使基材S1的不同區段被加熱至不同的溫度。加熱器111a~111c例如是紅外線輻射加熱器,但本發明並不限於此。As shown in FIGS. 1 and 2, the cyclic epitaxial deposition system M1 of the embodiment of the present invention further includes a
請參照圖1,抽氣裝置14是流體連通於主腔體10,以對主腔體10抽真空。抽氣裝置14,例如是一真空幫浦,可將主腔體10內的氣體抽出,以使主腔體10內部的壓力維持在一預定值。另外,抽氣裝置14設置在主腔體10下方,可抽走未吸附在基材S1上的前驅物氣體以及多餘的沖洗氣體。另外,本實施例的真空設備1還進一步包括一壓力溫度感測器15。壓力溫度感測器15設置在主腔體10內,可偵測主腔體10內的壓力以及溫度。Please refer to FIG. 1, the
請參照圖1,本發明實施例的循環式磊晶沉積系統M1還進一步包括設置在傳輸路徑上的一冷卻裝置16。據此,由鍍膜腔體11被傳送出的基材S1可被導引至冷卻裝置16。在本實施例中,冷卻裝置16為一設有冷卻管路的滾輪。基材S1由鍍膜腔體11被傳送至冷卻裝置16而被降溫之後,再被第二收放料模組13b收卷,但本發明不以此為限。在其他實施例中,冷卻裝置16也可以被省略。Please refer to FIG. 1, the circulating epitaxial deposition system M1 of the embodiment of the present invention further includes a
請配合參照圖1以及圖2,本發明實施例的循環式磊晶沉積系統M1還進一步包括氣體管路系統2、至少一前驅物儲存單元3、4以及惰性氣體儲存單元5、6。前驅物儲存單元3、4可通過氣體管路系統2,以供應前驅物氣體至其中一個前驅物氣體噴嘴110a、110c。相似地,惰性氣體儲存單元5也可通過氣體管路系統,以及供應沖洗氣體至沖洗氣體噴嘴110b。Please refer to FIG. 1 and FIG. 2 together, the circulating epitaxial deposition system M1 of the embodiment of the present invention further includes a
前驅物儲存單元3、4用以儲存用來反應的前驅物。在本實施例中,循環式磊晶沉積系統M1包括多個前驅物儲存單元3、4。另外,多個前驅物儲存單元3、4包括氣態前驅物儲存單元3以及液態前驅物儲存單元4的至少其中一者。The
詳細而言,氣態前驅物儲存單元3可包括多個氣瓶30、31,以分別儲存不同的前驅物氣體。液態前驅物儲存單元4可包括多個儲存槽40、41、42,以分別用以儲存不同的液態前驅物。當液態前驅物可通過加熱轉變為氣態,以輸出前驅物氣體至氣體分流模組110。惰性氣體儲存單元5可包括至少一氣瓶,以儲存惰性氣體。In detail, the gaseous
氣體管路系統2包括多個氣體主要管路20、21、22以及多個氣體分流管路200、210、220。每一氣體主要管路20、21、22通過對應的氣體分流管路200、210、220,以流體連通於對應的多個前驅物氣體噴嘴110a、110c或者沖洗氣體噴嘴110b。The
詳細而言,多個氣體主要管路20、21、22可包括前驅物氣體主要管路20、22以及惰性氣體主要管路21。多個氣體分流管路200、210、220可區分為前驅物氣體分流管路200、220以及惰性氣體分流管路210。據此,前驅物氣體主要管路20、22流體連通於對應的前驅物氣體分流管路200、220,而惰性氣體主要管路21是流體連通於對應的惰性氣體分流管路210。In detail, the multiple gas
氣態前驅物儲存單元3的氣瓶30、31或者是液態前驅物儲存單元4的儲存槽40、41、42流體連通於對應的前驅物氣體主要管路20、22,以輸送前驅物氣體。前驅物氣體並通過對應的前驅物氣體分流管路200、220而被輸送至氣體分流模組110。在本實施例中,多個前驅物氣體主要管路20、22可以分別輸送不同的前驅物氣體(第一前驅物氣體以及第二前驅物氣體)。The
惰性氣體儲存單元5的氣瓶會流體連通於惰性氣體主要管路21,以將惰性氣體輸入惰性氣體主要管路21內。惰性氣體並通過惰性氣體分流管路210,而流向氣體分流模組110。The gas cylinder of the inert gas storage unit 5 is fluidly connected to the inert gas
請參照圖1以及圖2,在本實施例中,氣體管路系統2還包括多個主流量控制閥20a、21a、22a以及多個分流控制閥200a、210a、220a。進一步而言,循環式磊晶沉積系統M1包括一控制模組(圖未示),且控制模組電性連接多個主流量控制閥20a、21a、22a以及多個分流控制閥200a、210a、220a。如圖1所示,多個主流量控制閥20a、21a、22a是分別設置在多個氣體主要管路20~22上。通過控制模組的控制,多個主流量控制閥20a、21a、22a可分別控制通過氣體主要管路20~22的前驅物氣體或是惰性氣體的流量。1 and 2, in this embodiment, the
如圖2所示,多個分流控制閥200a、210a、220a分別設置在多個氣體分流管路200、210、220上。通過控制模組的控制,多個分流控制閥200a、210a、220a可獨立地控制進入各個前驅物氣體噴嘴110a、110c的前驅物氣體的流量,以及進入沖洗氣體噴嘴110b的沖洗氣體的流量。As shown in Fig. 2, a plurality of flow dividing
在一實施例中,針對基材S1的其中一特定區域,通過分流控制閥200a、210a、220a的控制,可以改變每次鍍膜循環中,前驅物氣體以及沖洗氣體噴灑到該特定區域的順序。In one embodiment, for a specific area of the substrate S1, through the control of the
舉例而言,針對其中一氣體分流模組110,兩個第一前驅物氣體噴嘴110a中,只有其中一個第一前驅物氣體噴嘴110a內會通入第一前驅物氣體,而另一個第一前驅物氣體噴嘴110a內則不會被通入第一前驅物氣體。相似地,兩個第二前驅物氣體噴嘴110c中,只有其中一個第二前驅物氣體噴嘴110c內會通入第二前驅物氣體,而另一個第二前驅物氣體噴嘴110c內則不會被通入第二前驅物氣體。For example, for one of the
如此,當基材S1連續式地通過其中一氣體分流模組110下方時,基材S1的特定區域會依序接觸第一前驅物氣體、沖洗氣體、第二前驅物氣體以及沖洗氣體,從而形成另一種鍍膜循環。In this way, when the substrate S1 continuously passes under one of the
另外,氣體管路系統2還包括分別設置在多個氣體主要管路20~22上的多個預熱元件20b~22b。換句話說,每一個預熱元件20b~22b分別設置在對應的氣體主要管路20~22上。預熱元件20b~22b例如是加熱帶,可對通過氣體主要管路20~22內的前驅物氣體加熱,以避免前驅物氣體在進入氣體分流模組110之前被冷凝。In addition, the
[實施例的有益效果][Beneficial effects of the embodiment]
本發明的其中一有益效果在於,本發明所提供的循環式磊晶沉積系統M1,其能通過“輸送裝置13用以沿著一傳輸路徑連續地輸送一基材S1進出鍍膜腔體11”以及“氣體分流模組110包括彼此不連通的多個前驅物氣體噴嘴110a、110c以及多個沖洗氣體噴嘴110b,以在同一時間將至少一前驅物氣體以及至少一沖洗氣體分別導引至基材S1上的不同區域”的技術方案,以連續地在基材S1上形成膜層。One of the beneficial effects of the present invention is that the cyclic epitaxial deposition system M1 provided by the present invention can be used to continuously transport a substrate S1 in and out of the
本發明所提供的循環式磊晶沉積系統M1基本上仍是利用原子層沉積的原理來形成膜層。相較於現有的原子層沉積設備,本發明的循環式磊晶沉積系統M1也可精準地控制膜厚。利用本發明的循環式磊晶沉積系統M1所形成的膜層,也具有均勻性佳以及階梯覆蓋率高等優點。然而,利用本發明所提供的循環式磊晶沉積系統M1來形成膜層時,可縮短沉積時間,並適合應用於製造需要大量生產的元件或者裝置。The cyclic epitaxial deposition system M1 provided by the present invention basically still uses the principle of atomic layer deposition to form a film. Compared with the existing atomic layer deposition equipment, the cyclic epitaxial deposition system M1 of the present invention can also accurately control the film thickness. The film formed by the circulating epitaxial deposition system M1 of the present invention also has the advantages of good uniformity and high step coverage. However, when the cyclic epitaxial deposition system M1 provided by the present invention is used to form a film, the deposition time can be shortened, and it is suitable for manufacturing components or devices that require mass production.
以上所公開的內容僅為本發明的優選可行實施例,並非因此侷限本發明的申請專利範圍,所以凡是運用本發明說明書及圖式內容所做的等效技術變化,均包含於本發明的申請專利範圍內。The content disclosed above is only a preferred and feasible embodiment of the present invention, and does not limit the scope of the patent application of the present invention. Therefore, all equivalent technical changes made using the description and schematic content of the present invention are included in the application of the present invention. Within the scope of the patent.
M1:循環式磊晶沉積系統S1:基材1:真空設備10:主腔體11:鍍膜腔體110:氣體分流模組110a:第一前驅物氣體噴嘴110b:沖洗氣體噴嘴110c:第二前驅物氣體噴嘴P1:第一前驅物氣體分布區P2:第二前驅物氣體分布區P3:沖洗氣體分布區111:加熱模組111a~111c:加熱器12:前處理腔體120:電漿裝置121:前處理加熱模組13:輸送裝置13a:第一收放料模組13b:第二收放料模組14:抽氣裝置15:壓力溫度感測器16:冷卻裝置2:氣體管路系統20、22:前驅物氣體主要管路20a、21a、22a:主流量控制閥20b、21b、22b:預熱元件21:惰性氣體主要管路200、220:前驅物氣體分流管路210:惰性氣體分流管路200a、210a、220a:分流控制閥3:氣態前驅物儲存單元30、31:氣瓶4:液態前驅物儲存單元40、41、42:儲存槽5、6:惰性氣體儲存單元d:最短垂直距離M1: Circulating epitaxy deposition system S1: substrate 1: vacuum equipment 10: main chamber 11: coating chamber 110:
圖1為本發明循環式磊晶沉積系統的示意圖。Fig. 1 is a schematic diagram of the cyclic epitaxial deposition system of the present invention.
圖2為本發明實施例的氣體分流模組的示意圖。Fig. 2 is a schematic diagram of a gas distribution module according to an embodiment of the present invention.
M1:循環式磊晶沉積系統 M1: Circulating epitaxial deposition system
S1:基材 S1: Substrate
1:真空設備 1: Vacuum equipment
10:主腔體 10: Main cavity
11:鍍膜腔體 11: Coating cavity
110:氣體分流模組 110: Gas splitter module
110a:第一前驅物氣體噴嘴 110a: First precursor gas nozzle
110b:沖洗氣體噴嘴 110b: flushing gas nozzle
110c:第二前驅物氣體噴嘴 110c: second precursor gas nozzle
111:加熱模組 111: Heating module
111a~111c:加熱器 111a~111c: heater
12:前處理腔體 12: Pretreatment chamber
120:電漿裝置 120: Plasma device
121:前處理加熱模組 121: Pre-treatment heating module
13:輸送裝置 13: Conveying device
13a:第一收放料模組 13a: The first retractable module
13b:第二收放料模組 13b: The second retracting and unwinding module
14:抽氣裝置 14: Air extraction device
15:壓力溫度感測器 15: Pressure and temperature sensor
16:冷卻裝置 16: Cooling device
2:氣體管路系統 2: Gas pipeline system
20、22:前驅物氣體主要管路 20, 22: Main pipeline of precursor gas
200、220:前驅物氣體分流管路 200, 220: precursor gas shunt pipeline
210:惰性氣體分流管路 210: Inert gas bypass line
20a、21a、22a:主流量控制閥 20a, 21a, 22a: main flow control valve
20b、21b、22b:預熱元件 20b, 21b, 22b: preheating element
21:惰性氣體主要管路 21: Inert gas main pipeline
3:氣態前驅物儲存單元 3: Gaseous precursor storage unit
30、31:氣瓶 30, 31: cylinder
4:液態前驅物儲存單元 4: Liquid precursor storage unit
40、41、42:儲存槽 40, 41, 42: storage tank
5、6:惰性氣體儲存單元 5, 6: Inert gas storage unit
Claims (16)
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TW108119349A TW202045753A (en) | 2019-06-04 | 2019-06-04 | Cyclic epitaxy deposition system |
CN202010106115.4A CN112030139A (en) | 2019-06-04 | 2020-02-20 | Circulating epitaxial deposition system |
US16/862,760 US20200385885A1 (en) | 2019-06-04 | 2020-04-30 | Cyclical epitaxial deposition system |
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TW108119349A TW202045753A (en) | 2019-06-04 | 2019-06-04 | Cyclic epitaxy deposition system |
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US20230047186A1 (en) * | 2021-08-13 | 2023-02-16 | Nano-Master, Inc. | Apparatus and Methods for Roll-to-Roll (R2R) Plasma Enhanced/Activated Atomic Layer Deposition (PEALD/PAALD) |
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US8084682B2 (en) * | 2009-01-21 | 2011-12-27 | Yung-Tin Chen | Multiple band gapped cadmium telluride photovoltaic devices and process for making the same |
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